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对浮动床生物膜硝化反应器的研究 被引量:1

A Study on the Moving Bed Nitrifying Biofilm Reactor
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摘要 以氨氮的硝化为目的 ,对浮动床生物膜硝化反应器采用具有表面积大 ,不易堵塞的新型载体填装进行试验。研究表明 :在碱度过剩且不存在有机负荷的条件下 ,硝化反应速率或是由氧的浓度决定或是由氨氮的浓度决定。当氧的浓度为硝化反应限速因素时 ,氧的浓度对硝化反应速率有很大影响 ,当氧的浓度达到 4 .5 mg/ l时 ,硝化反应速率可达到 2 4 0 g NOx- N/ m3· A new biofilm reactor moving bed reactor which is filled with carriers bearing high specific surface and less possibilities of clogging is studied.The experiment results show that when alkalinity is in excess and there is no organic load, the nitrification rate can be determined either by the ammonium concentration or by the oxygen concentration.We have found that the oxygen concentration imposes a great influence on the nitrification rate when oxygen becomes a rate limiting factor.When the oxygen concentration is about 4.5mg/l, the nitrification rate can reach at 240gNOx N/m 3·d.
出处 《桂林电子工业学院学报》 2003年第1期31-33,共3页 Journal of Guilin Institute of Electronic Technology
关键词 浮动床 生物膜 硝化反应器 反应动力学 有机负荷 污水处理 biofilm, nitrification, moving bed, kinetics, organic load
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参考文献3

  • 1[1]Lars J Hem.Nitrification in moving bed biofilm reactor[J]. Water Research,1999,(6):1425-1433.
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  • 2胡明成,龙腾锐.含硫酸盐废水厌氧处理过程中底物的竞争[J].桂林电子科技大学学报,2006,26(5):390-394. 被引量:14
  • 3DAVID POLLARD. Screening of Bioftocculant Producing Microbes U. filifing Fatty Acids and their Porperties of Producing Flocculates [C]//IBS Biomine 1997 Symposium, Sydney, Australia, 1997 :4-6.
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  • 8ZHOU Q X,SHI J H. Elects of smalhown construction on the utilization and cycles of water resources and relevant ecological countermeasuers [G]//Researeh on and Probe into Ecology. Beijing : China Environmental Science Press, 1997, Z95-Z99.
  • 9崔福义,张霄宇,冯琦,周波,周富涛.常规水处理混凝沉淀工艺中除浊与除铝的相关性研究[J].哈尔滨建筑大学学报,2002,35(3):52-55. 被引量:13

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